BACKGROUND OF THE INVENTION
[Field of the Invention]
[0001] The objects of this invention are to offer alkaline-manganese batteries or lithium-ion
secondary batteries using the powder of manganese oxides consisting of manganese dioxide
or double oxide of manganese and lithium on which a surface modification layer is
formed as a positive active material, and a manufacturing method of said positive
active materiel for the batteries made-of manganese oxide powder on which a surface
modification layer is formed.
[Description of the Prior Arts]
[0002] Various primary batteries employing manganese dioxide as the positive active material
such as the carbon-zinc dry batteries called Leclanche type or zinc chloride type
batteries employing neutral salts of ammonium chloride or zinc chloride as electrolyte,
alkaline manganese batteries employing potassium hydroxide as the electrolyte, and
Li/MnO
2 system primary batteries belonging to organic electrolyte lithium batteries employing
manganese dioxide as the positive active material have been known well.
[0003] On the other hand, lithium-ion secondary batteries which can be high-energy density
small size rechargeable batteries in next generation have been known also. These batteries
employ positive and negative electrodes made of a host material repeating intercalation
and deintercalation of lithium-ions by charging and discharging realizing the heavy
load discharge, rapid charge, long cyclic life, etc.
[0004] Presently, as the host material, a double oxide consisting of cobalt and lithium,
or LiCoO
2, is used as the positive electrode, while carbon is generally used as the negative
electrode. However, because of the unstable world supply comes from the high cost
and omnipresence of positive electrode material or cobalt, this is now to be substituted
by LiMnO
2 or LiMn
2O
4 which is a double oxide of manganese and lithium.
[0005] As the result of recent power consumption decrease realized by the significant advancement
of semiconductor electronics technology, a number of portable electric and electronic
apparatuses have been developed and practically used. Various AV apparatuses including
the strobe-flash light for still-camera, portable shaver, headphone stereo-player,
and LCD-TV are typical of these advancements wherein the demand and the use of alkaline
manganese batteries having excellent continuous discharge characteristics are now
expanding very rapidly.
[0006] However, in contrast to these tendencies, increases of power consumption by the multi-functioned
portable apparatuses have been obvious. For example, in the cases of PDA such as portable
telephone and facsimile, note-type personal computer and cam-coder, better battery
performances taking heavy and continuous loads have been demanded.
[0007] Therefore, new built-in type secondary batteries such as the high-capacity nickel-cadmium
system, nickel-metal hydride system, or lithium ion type batteries have been developed.
And, at the same time, the demands for alkaline manganese batteries capable of continuous
discharge at heavy load working as supplementary power source are increasing.
[0008] When batteries are continuously discharged, decreases of operating voltages due to
the polarization are generally inevitable in proportion to the increase of load current.
Thus, the end voltage is reached before the active materials of positive and negative
electrode are fully reacted so that the ultimate efficiency of active material remains
low.
[0009] The polarization lowering of the operation voltage of discharging cell could be attributed
for three reasons including the resistance polarization due to the electrical ohmic
resistance produced in the outer and inner cell, the activation polarization due -to
the charge transfer reaction, and the concentration polarization due to the diffusion
control process of reaction substance or products.
[0010] Conventionally, in order to improve the continuous heavy load discharge characteristics
of alkaline manganese batteries, the amount of electrolytic manganese dioxide (herein-after,
abbreviated as EMD) contained in the positive active material has been increased,
a high conductivity graphite is used as the conductive material in the positive electrode
mix lowering the amount of additives, or a thin separator in which very fine fibers
are uniformly distributed has been employed.
[0011] Other than these, improvements introducing a gelling agent or a zinc corrosion inhibitor
in the negative electrode have been considered effective. Beside this, the employment
of a positive electrode of larger polarization in compared to the zinc in the negative
electrode has been considered also.
[0012] For example, as shown in U.S. Patents 5,277,890 and 5,391,365, methods using EMD
powder expanding its specific surface by forming filament-like protrusions thereon
by using a chemical synthetic method precipitating MnO2 thereon had been developed.
Beside this, a method using a positive electrode to which powder of anatase titanium
dioxide is added and mixed as shown in U.S. Patent 5,342,712 had been disclosed.
[0013] Although these inventions had been slightly effective increasing the battery service-life
at continuous discharge decreasing the polarization comparing over a case where a
conventional positive electrode made of EMD powder only is used, these had been effective
very little when a heavier load has to be discharged continuously.
[0014] The objects of this invention are to offer alkaline-manganese batteries or lithium-ion
secondary batteries having longer service lives at heavier load and continuous discharge,
and these are made of powder of manganese oxides employing manganese dioxide or double
oxide of manganese and lithium on which surface modification layers acting as the
positive active material are formed, and a manufacturing method of the positive active
materiel for these batteries.
SUMMARY OF THE INVENTION
[0015] Though some of the typical improvements of heavy load continuous discharge characteristics
of conventional alkaline-manganese batteries have been described so far, most of these
are related to the positive electrode of relatively large polarization. The present
invention has been proposed from a similar point of view.
[0016] Mainly, MnO
2 powder or highly active EMD powder is used as the positive active material of alkaline
manganese batteries in most of the cases. Since the electronic conductivity of EMD
powder is not necessarily be very high, a conductive agent consisted mainly of graphite
having no direct contribution to its conductivity had to be added up to an amount
of 10 wt%.
[0017] The main discharge reaction of MnO
2 acting as the positive active material in the alkaline electrolyte can be expressed
by a uniform solid-phase reaction shown in Eq. (1), wherein not only the improvement
of conductivity of active material but the employment of the material minimizing the
concentration polarization due to the ion diffusion within the solid phase are desirable.

[0018] The positive electrode potential is expressed by Eq. (2).

[0019] As shown in above, the present invention is to offer batteries having excellent continuous
discharge characteristics realized before even when a heavy load is applied, by employing
manganese oxide consisting of EMD powder of which surface is suitably modified as
the positive active material having a very little ohmic loss due to the electric resistance
and having a small concentration polarization particularly.
[0020] More concretely, the objects of the invention are accomplished by batteries employing
a positive active material consisting of manganese oxide powder having a surface modified
by depositing a layer of compound consisting mainly of oxide of at least one element
selected out of a group of titanium (Ti), cobalt (Co), nickel (Ni), strontium (Sr),
and lanthanum (La) thereon.
BRIEF DESCRIPTION OF THE DRAWINGS
[0021] Fig. 1 shows a flow-chart of manufacturing process of the invented positive active
material consisting of manganese oxide having a surface modified layer.
[0022] Fig. 2 shows examples of comparative transition curves of single electrode potentials
of positive active materials made of surface modified by present invention and conventional
untreated EMD powder placed in an alkaline electrolyte.
[0023] Fig. 3 shows a relationship between the amount of titanium contained in the invented
EMD powder of which surface is modified, the electric conductivity, and the gravimetric
capacity density thereof.
[0024] Fig. 4 shows a half vertical cross-section of LR6(AA) size alkaline manganese battery
which is a typical example of the invented battery.
[0025] Fig. 5 are drawings comparing the discharge characteristics of alkaline manganese
batteries employing invented positive active material having a surface layer modified
by nickel compound with the one obtained by employing conventional positive active
material made of untreated EMD powder.
[0026] Fig. 6 shows a relationship between the total amount of Co and/or Ni contained in
the modified surface layer of EMD powder and the discharge capacity ratio.
[0027] Fig. 7 shows a discharge characteristics of alkaline manganese battery employing
invented positive active material having a surface layer modified by La compound,
compared with the one obtained by employing a positive active material using conventional
untreated EMD powder.
[0028] Fig. 8 shows a relationship between the total amount of Sr and/or La contained in
the surface modified layer of EMD powder and the possible number of pulse discharges.
[0029] Fig. 9 shows a cross-sectional view of coin type lithium ion secondary cell which
is an other typical example of the invented battery.
[0030] Fig. 10 shows a cross-sectional view of R20(D) size zinc chloride type carbon-zinc
dry cell which is an other typical example of the invented battery.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0031] A typical structure of the invented alkaline manganese battery and a manufacturing
method of the positive active material for the same are now explained here by referring
the attached drawings and tables.
<Embodiment-1>
[0032] The EMD block electrodeposited on a Ti anode held in a high-temperature manganese
sulphate bath kept at a temperature of more than 90°C is peeled off first from the
Ti anode. After coarsely crashing and washing the blocks of EMD, this is pulverized
by a roller-mill obtaining EMD powder having an average grain diameter of 50 µm, and
this is dried by a conventional method before obtaining EMD powder.
[0033] After this, The surface of EMD powder is subjected to a modification treatment according
to the flow-chart of manufacturing process shown in Fig. 1.
(1) Mixing ...Weighing 300 grams of the EMD powder, this is mixed in an aqueous solution
of 3.0 liters containing titanium sulfate of neutral or H2SO4 acidity and is dispersed.
(2) Treatment ... By heating the solution holding said EMD powder in a dispersed condition,
Ti compound is deposited and coated on the surface of EMD powder modifying the surface
thereof. A treatment temperature of 80°C is used in this case. The treatment can be
accelerated by bubbling the oxidizing gas such as air, oxygen, or ozone containing
the air or oxygen into the solution, or by adding an oxidizing agent such as sodium
perchlorate (NaClO3) or sodium persulfate (Na2S2O8 .2H2O) thereto.
(3) Filtration ...The EMD powder of which surface is modified is filtrated in this
process, and this process may be replaced by a decantation of the supernatant solution,
and this is shifted into the succeeding washing process.
(4) Washing ...Pouring and stirring of pure water, and removal of the supernatant
solution is repeated for several times.
(5) Neutralization ...By dropping sodium hydroxide aqueous solution in a state of
agitation, the pH thereof is stabilized into a range from 6.0 to 8.0.
(6) Drying...The product is dried for 24 hours at 80°C.
[0034] Beside above, the surface modification shown in the processes of (1) - (3), may be
replaced by processes of coarse crushing of EMD grain, (4) Washing, (5) Neutralization,
and a process of Pulverizing. Furthermore, stabilization and improvements of characteristics
of modified EMD are possible by applying a heat treatment in a sulfuric acid aqueous
solution after Treatment of (2).
[0035] The electric conductivity, moistures, and the discharge capacity ratios of positive
active materials determined by changing the addition of sulfuric acid (H
2SO
4) to Ti(SO
4)
2 aqueous solution and the type of oxidizing agent are listed in Table 1 shown below.
Table-1
| Sample No. |
1 |
2 |
3 |
4 |
5 |
6 |
7 |
8 |
9 |
10 |
11 |
| Composition of Treatment Solution |
|
|
|
|
|
|
|
|
|
|
|
| Ti(SO4)2(mol/1) |
- |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
- |
0.2 |
0.2 |
0.2 |
| H2SO4 (mol/1) |
- |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
- |
- |
- |
| Oxidizing Agent |
|
|
|
|
|
|
|
|
|
|
|
| Air (ml/min) |
- |
- |
- |
- |
50 |
- |
- |
- |
- |
50 |
- |
| O2 (ml/min) |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
- |
- |
| O3 (ml/min) |
- |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
- |
| Na2ClO3 |
- |
○ |
- |
- |
- |
- |
- |
- |
○ |
- |
- |
| Na2S2O82H2O |
- |
- |
○ |
- |
- |
- |
- |
- |
- |
- |
- |
| Electric Conductivity (x10-3S/cm) |
13.7 |
995 |
990 |
800 |
930 |
950 |
950 |
14.0 |
810 |
870 |
570 |
| Moisture(wt%) |
4.58 |
4.90 |
4.80 |
4.20 |
4.55 |
4.35 |
4.43 |
4.12 |
4.05 |
4.32 |
4.55 |
| Discharge Capacity Ratio |
100 |
107 |
106 |
105 |
107 |
107 |
106 |
101 |
105 |
106 |
104 |
[0036] In Table 1, the ozone (O
3) content in the oxidizing agent means direct bubbling of oxygen (O
2). including the O
3 generated by the flow-in of O
2 into the ozonizer at a flow rate of 50 ml/min into the treatment solution.
[0037] The electric conductivity is determined by placing the sample powder of predetermined
volume in a die made of PTFE, and by measuring the terminal DC resistance at a state
where a pressure of 3t/cm
2 is applied. The moisture is determined by reducing the weight of sample heated and
dehydrated at 500°C from the weight of sample dried at 105°C.
[0038] In addition to these, preparing a working positive electrode by pressing a mixture
of sample powder of 10 weight part mixed with acetylene black of 1 weight part on
to a platinum (Pt) plate, using a counter electrode made of Pt plate and a reference
electrode made of Hg/HgO, and by measuring the capacity of the positive electrode
potential reaching to a potential of -300 mV from the reference electrode potential
applying a constant current of 10 mA per one gram of the sample in an alkaline electrolyte
consisting of 40 wt% potassium hydroxide (KOH) aqueous solution dissolving 3.0 wt%
zinc oxide (ZnO), and the capacity ratios of each sample are derived defining the
capacity of the EMD powder sample No. 1 as 100.
[0039] In here, the discharge end potential of -300 mV is employed as a potential corresponding
to the discharge ending voltage of alkaline manganese battery which is 0.9 V.
[0040] Table 1 shows that all of the electric conductivity of Samples Nos. 2 - 7 and Nos.
9 - 10 obtained by treating the EMD powder in a Ti(SO
4)
2 aqueous solution are higher by about two orders comparing to that of untreated EMD
powder Sample No. 1. Among these, tendencies of slightly higher electric conductivity
are observed when H
2SO
4 is added to the treatment solution (Sample Nos. 2 - 7). These tendencies are obvious
particularly when H
2SO
4 is added together with the oxidizing agent (Sample Nos. 2, 3, 5, 6, and 7). In addition
to these, no particular differences depending on the type of oxidizing agent have
been observed.
[0041] The electron-microscopic observations made on the surfaces of untreated EMD powder
of Sample No. 1 and those of Sample No. 2 obtained by treating the EMD powder in a
H
2SO
4 acidity Ti(SO
4)
2 aqueous solution being added by an Na
2ClO
3 oxidizing agent, proved a little surface irregularity of Sample No. 1 while less
irregularities on Sample No. 2 which could attributed for the irregularities smoothed
out by the deposition.
[0042] Since a moisture up to 5 wt.% is contained in EMD powder usually, the content of
MnO
2 and the electric conductivity could be increased by the removal of moisture which
could be done by applying a heat treatment. However, sacrificing the capacity on the
other hand by the positive electrode potential lowered by the discharge in the alkaline
electrolyte.
[0043] Table 1 proves that not only the electric conductivity improved by two orders but
the significantly increased discharge capacity can be obtained without reducing the
moisture by using the EMD powder on which a surface modified layer is formed by using
a Ti compound,
[0044] It has been confirmed that the content of titanium in Sample No. 2 is close to 1.8
wt.% by using an element analysis method. Thus, this is attributed for the EMD powder
of which entire or partial surface is modified by the thin deposition of titanium
compound consisting mainly of titanium oxide. Although the exact determination of
the thickness of surface modified layer is found impossible because of its extremely
thin thickness even with an X-ray diffraction method. However, the effectiveness of
the surface modified layer is obvious.
[0045] Fig. 2 shows two discharge characteristics of unipolar electrode potential in an
alkaline electrolyte obtained with Sample Nos. 1 and 2.
[0046] In Fig. 2, while a rapid potential decrease of Sample No. 1 employing untreated EMD
powder at the ending of discharge is observed, a gentle potential decrease of Sample
No. 2 employing the EMD powder on which a surface layer modified by a titanium compound
is found, and this could be attributed for the significant capacity improvement thereof.
In addition to this, no particular effect of surface modification has been observed
with Sample No. 8 employing the EMD powder treated by sulfuric acid, and very little
change with Sample No. 1 is observed.
<Embodiment-2>
[0047] Fixing the concentration of sulfuric acid in the treatment solution at 2.0 mol/l,
various surface modified EMD powders of different titanium contents are prepared in
accordance to Embodiment-1 changing the concentration of Ti(SO
4)
2 and the treatment condition.
[0048] From these, the gravimetric capacity densities (mAh/g) are determined from the measurements
of electric conductivity and the single electrode discharge tests, and the results
of these are shown in Fig. 3.
[0049] Fig. 3 shows also a steady increase of the electric conductivity in proportion to
the increase of Ti content in contrast to that of Sample No. 1 which is fixed at 13.7
x 10
-3 S/cm, and shows also a near saturation of electric conductivity at a point exceeding
0.1 wt.%. On the other hand, the gravimetric capacity density is found optimum in
a range of titanium content from 0.1 - 5.0 wt.%.
<Embodiment-3>
[0050] Various positive active materials of which surfaces are modified are prepared by
adding salts of manganese, nickel, or cobalt to the H
2SO
4 acidity Ti(SO
4)
2 treatment solution according to the case of Embodiment-1, and the electric conductivity,
moistures, and the apparent densities thereof are measured. Then, preparing various
LR6(AA) type alkaline manganese batteries, the discharge capacity ratios at heavy
and medium loads are determined.
[0051] A cross-section of experimental LR6 size alkaline manganese battery is shown in Fig.
4 wherein the cap 1A made of nickel plated steel acting its positive terminal is integrally
molded-, and conductive coating 1B made of carbon paint is coated on the inner wall
of the positive can 1.
[0052] Then, manganese oxide made either of untreated EMD powder or various surface modified
EMD powder mixed with graphite at a weight ratio of 9 to 1 is press-molded into a
shape of cylinder, and four of the cylinders are inserted into said positive can 1,
and positive electrode mold 2 is press- molded on the inner wall of positive can 1.
[0053] Inserting cylinder-shaped separator 3 and bottom plate 3A within positive electrode
mold 2, gel negative electrode 4 prepared by dispersing the zinc powder of 2 weight
part in a viscose solution of 1 weight part dissolving a gelling agent made of carboxymethyl
cellulose (CMC) or polysodium acrylate or others into said alkaline electrolyte is
injected.
[0054] Then, negative electrode terminal 6 made of nickel-plated steel on which brass current
collector 5 is welded and washer 7 are integrated by plastic sealer 8, and this unit
is inserted into gel negative electrode 4. At a condition where sealer 8 is placed
on groove 1C formed by inwardly curling the opening of positive can 1, the upper edge
of said can 1 is curled inwardly sealing the can. This cell assembly process is ended
by sticking label 9 thereon at the end.
[0055] The discharge test of each cell is performed under a heavy load giving a constant
current of 1000 mA and under a medium load giving a constant resistance of 10 ohms
continuous discharge, obtaining a discharge-end voltage of 0.9 V in both cases. Table
1 shows a tabulation of discharge periods where the discharge period obtained by Sample
No. 1 cell employing a positive active material made of untreated EMD powder is defined
as 100, and the ones of other cells each employing positive active material made of
treated EMD powder of which surface layer is modified are defined as the ratios of
those to that of Sample No. 1.
[0056] The results of these are tabulated in Table 2.
Table 2
| Sample No. |
1 |
2 |
12 |
13 |
14 |
15 |
16 |
17 |
18 |
19 |
20 |
| Composition of Treatment Solution |
|
|
|
|
|
|
|
|
|
|
|
| Ti(SO4)2(mol/l) |
- |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
| H2SO4(mol/l |
- |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
| MnSO4(mol/l) |
- |
- |
0.2 |
- |
- |
0.2 |
0.2 |
- |
0.2 |
0.2 |
0.2 |
| CoSO4(mol/l) |
- |
- |
- |
0.2 |
- |
0.2 |
- |
0.2 |
0.2 |
0.2 |
0.2 |
| NiSO4(mol/l) |
- |
- |
- |
- |
0.2 |
- |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
| Kind of Oxidizing Agent |
|
|
|
|
|
|
|
|
|
|
|
| Air (ml/min) |
- |
- |
- |
- |
- |
- |
- |
- |
- |
50 |
- |
| O2 (ml/min) |
- |
- |
- |
- |
- |
- |
- |
- |
- |
- |
50 |
| Na2ClO3 |
- |
o |
o |
o |
o |
o |
o |
o |
o |
- |
- |
| Electric Conductivity |
|
|
|
|
|
|
|
|
|
|
|
| (x10-3S/cm) |
13.7 |
995 |
990 |
990 |
930 |
950 |
950 |
950 |
970 |
980 |
920 |
| Moisture(wt.%) |
4.58 |
4.9 |
4.2 |
4.2 |
4.55 |
4.15 |
4.13 |
4.12 |
4.05 |
4.12 |
4.15 |
| Apparent Density(g/cm3) |
|
|
|
|
|
|
|
|
|
|
|
| |
2.67 |
2.60 |
2.92 |
2.65 |
2.66 |
2.93 |
2.90 |
2.64 |
2.96 |
2.87 |
2.89 |
| Heavy load Discgarge Capacity Ratio |
|
|
|
|
|
|
|
|
|
|
|
| |
100 |
100 |
100 |
105 |
105 |
103 |
103 |
105 |
105 |
105 |
105 |
| Medium Load Discharge Capacity Ratio |
|
|
|
|
|
|
|
|
|
|
|
| |
100 |
107 |
106 |
105 |
105 |
107 |
106 |
102 |
105 |
106 |
104 |
[0057] While the electric conductivity of untreated EMD powder of Sample No. 1 is 13.7 x
10
-3S/cm, those of the others using the treatment which includes titanium salt solution
containing either the salt of manganese, nickel, cobalt, etc., are higher by two orders.
Moistures of Sample Nos. 12, 15, 16, 18, 19 and 20 added with manganese salt are found
slightly less than that of Sample No. 1, and a slight increase of the apparent densities
is found also.
[0058] These could be attributed for a possible deposition of chemical manganese dioxide
(CMD) having a fundamentally low moisture (less than 1.0%) on EMD simultaneously with
the deposition of a compound consisting mainly of titanium oxide.
[0059] Considerably improved heavy load discharge characteristics are found with Sample
Nos. 13 - 20 depositing a cobalt and/or nickel compound mixed with a titanium compound.
Said considerable improvements of heavy load discharge characteristics can not be
explained only by the nobler potential of CoOOH and/or NiOOH of cobalt and/or nickel
oxide deposited together with the titanium oxide, but it could be probably explained
by the suppressed concentration polarization together with the suppressed resistance
polarization took place during the discharge.
[0060] Moreover, since the electric conductivity of surface modified EMD including the titanium
compound is improved, the content of conductive agent such as graphite could be reduced
at a level less than 10 wt.%. However, the dependency on the type of oxidizing agents
has not been clarified.
<Embodiment-4>
[0061] In Embodiment-3 described before, the improvements of heavy load discharge characteristics
of alkaline manganese batteries by employing the EMD powder of which surface is modified
by a titanium compound together with a compound of cobalt and/or nickel compound and
the cobalt and/or nickel compound including the manganese compound has been explained.
[0062] Therefore, in Embodiment-4 shown here, LR6 size alkaline manganese batteries utilizing
a positive active material formed on the EMD powder of which surface layer is modified
are prepared in accordance to Embodiemnt-1 using a solution of cobalt salt and/or
nickel salt, or cobalt salt and/or nickel salt including the manganese salt excluding
the use of titanium salt in the treatment solution.
[0063] All of these batteries are subjected to a continuous discharge test supplying a constant
current of 1500 mA (obtaining an end voltage of 0.9 V), and the discharge capacity
ratios of those batteries defining that obtained by Sample No.1 using untreated EMD
powder as 100 are determined. The results of those are shown in Tables 3, 4, and 5.
Table 3
| Sample No. |
1 |
21 |
22 |
23 |
24 |
25 |
26 |
27 |
28 |
29 |
| Composition of Treatment Solution |
|
|
|
|
|
|
|
|
|
|
| H2SO4 (mol/1) |
- |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
- |
- |
- |
| CoSo4 (mol/l) |
- |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
| Oxidizing Agent |
|
|
|
|
|
|
|
|
|
|
| Air (ml/min) |
- |
- |
- |
- |
50 |
- |
- |
- |
- |
50 |
| O2 (ml/min) |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
- |
| O3 (ml/min) |
- |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
| Na2ClO3 |
- |
- |
o |
- |
- |
- |
- |
- |
o |
- |
| Na2S2O8.2H2O |
- |
- |
- |
o |
- |
- |
- |
- |
- |
- |
| Discharge Capacity Ratio |
|
|
|
|
|
|
|
|
|
|
| |
100 |
104 |
106 |
106 |
105 |
104 |
106 |
104 |
104 |
106 |
Table 4
| Sample No. |
1 |
30 |
31 |
32 |
33 |
34 |
35 |
36 |
37 |
38 |
| Composition of Treatment solution |
|
|
|
|
|
|
|
|
|
|
| H2SO4(mol/l |
- |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
- |
- |
- |
| NiSO4(mol/l) |
- |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
| Kind of Oxidizing Agent |
|
|
|
|
|
|
|
|
|
|
| Air (ml/min) |
- |
- |
- |
- |
50 |
- |
- |
- |
- |
50 |
| O2 (ml/min) |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
- |
| O3 (ml/min) |
- |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
| Na2ClO3 |
- |
- |
o |
- |
- |
- |
- |
- |
o |
- |
| Na2S2O8.2H2O |
- |
- |
- |
o |
- |
- |
- |
- |
- |
- |
| Discharge Capacity Ratio |
|
|
|
|
|
|
|
|
|
|
| |
100 |
105 |
107 |
106 |
107 |
107 |
106 |
104 |
105 |
106 |
Table 5
| Sample No. |
1 |
39 |
40 |
41 |
42 |
43 |
44 |
45 |
46 |
47 |
48 |
| Composition of Treatment Solution |
|
|
|
|
|
|
|
|
|
|
|
| H2SO4 (mol/1) |
- |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
- |
- |
| CaSO4 (mol/l) |
- |
0.2 |
- |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
| NiSO4 (mol/1) |
- |
0.2 |
0.2 |
- |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
| MnSO4 (mol/1) |
- |
- |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
- |
0.2 |
| Oxidizing Agent |
|
|
|
|
|
|
|
|
|
|
|
| Air (ml/min) |
- |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
- |
| O2 (ml/min) |
- |
- |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
| O3 (ml/min) |
- |
- |
- |
- |
- |
- |
- |
- |
50 |
- |
- |
| Na2ClO3 |
- |
o |
o |
o |
o |
- |
- |
- |
- |
- |
- |
| Na2S2O8.2H2O |
- |
- |
- |
- |
- |
o |
- |
- |
- |
- |
- |
| Apparent density(g/cm3) |
2.67 |
2.65 |
3.03 |
2.98 |
2.92 |
2.92 |
2.97 |
3.00 |
3.01 |
2.66 |
2.88 |
| Discharge Capacity Ratio |
|
|
|
|
|
|
|
|
|
|
|
| |
100 |
106 |
105 |
105 |
106 |
107 |
106 |
107 |
105 |
104 |
105 |
[0064] Respective examples of 1500 mA constant current continuous discharge characteristics
of alkaline manganese battery using the positive active material employed by Sample
No. 1 and Sample No. 30 are shown in Fig. 5.
[0065] Fig. 5 shows a higher discharge capacity up to a discharge end voltage of 0.9 V since
the discharge voltage is improved by using EMD powder of which surface layer is modified
by a nickel compound made- mainly of nickel oxide which could be NiOOH used as the
positive electrode.
[0066] Beside this, no noticeable difference between the points at which the discharge capacity
is lost and the discharge voltage is rapidly decreased have been observed.
[0067] In the cases where the surface of EMD powder is modified by introducing a Co and/or
Ni compound or a Co and/or Ni compound containing a Mn compound into the treatment
solution, tendencies realizing a slightly higher discharge voltage and discharge capacity
ratio have been observed when the treatment solution of H
2SO
4 acidity (Samples Nos. 21 - 26, 30 - 35, and 39 - 46) is used compared with the case
where the treatment solution of no H
2SO
4 acidity is used.
[0068] Moreover, though no particular effect of the oxidizing agent type have been observed
in this case, slightly improved discharge characteristics realized by the introduction
of an any oxidizing agent in the treatment process have been seen.
[0069] In this embodiment also, like the case of Embodiment-3, the higher apparent density
realized by the introduction of manganese salt in the treatment solution have been
observed.
[0070] Fig. 6 shows a relationship between the discharge capacity ratio of positive electrode
made of EMD powder of which surface is modified by the deposition of Co and/or Ni
compound and the total contents of Co and/or Ni. Like the cases of Embodiments-1 and
-2, the discharge capacity ratios are determined by conducting single electrode discharge
tests in an alkaline electrolyte and defining the one obtained by the untreated END
powder as 100. Fig. 6 shows also the discharge capacity ratios of every EMD powder
of which surface layers are modified by using a Co and/or Ni compound, and these are
higher than that (240 mAh/g) of untreated EMD powder. Note is the effectiveness of
total contents of Co and/or Ni in a range from 0.1 - 10.0 wt%. in these cases.
[0071] Electron-microscopic observations made on the surface of EMD powder modified by a
Co and/or Ni compound and a Co and/or Ni compound containing a Mn compound, like the
case where the surface is modified by a Ti compound, has proved the order of surface
irregularities less than those observed on the untreated EMD powder. Moreover, like
the cases of Embodiments -3 and -4, the higher apparent densities of surface modified
EMD powder containing a Mn compound (Sample Nos. 40 - 46 and 48) are observed.
<Embodiment-5>
[0072] The Embodiments -1 - -4 have proved the effectiveness of EMD powder of which surfaces
are modified by forming a Ti compound or a Co (cobalt) and/or Ni (nickel) compound
and by forming a Ti compound containing Mn or Co and/or Ni compound. In this Embodiment-5,
the effects of the surface modification by using a Sr (strontium) and/or La (lanthanum)
compound, and by using a Sr (strontium) and/or La (lanthanum) compound containing
Mn compound are confirmed.
[0073] Like the case of Embodiment-1, various LR6-size alkali manganese batteries employing
the EMD powder of which surface is modified by a Sr (strontium) and/or La (lanthanum)
compound, and by a Sr (strontium) and/or La (lanthanum)compound containing a Mn compound
as its positive active material are prepared, and these are subjected to a pulse discharge
test.
[0074] The pulse discharge test is a test simulating a strobe flash for still-camera where
the discharge is repeated for a 15 sec., on a constant resistance of 1.8 ohm allowing
a rest period of 45 sec., are the number of the discharges is counted until an end
voltage of 0.9 V is reached. Defining the number of pulse discharges obtained by the
cell of Sample No. 1 employing untreated EMD powder is 100, the ratio of the number
of pulse discharges obtained by a cell employing surface modified EMD powder is expressed
by the discharge capacity ratio. These results are shown in Tables 6, 7, and 8.
[0075] Some examples of the 1500 mA constant current discharge characteristics of LR6-size
alkaline manganese batteries prepared by employing untreated EMD powder, and the ones
employing the positive active material employing the EMD powder (Sample No. 58) of
which surface is modified by a La compound are shown in Fig. 7.
Table 6
| Sample No. |
1 |
49 |
50 |
51 |
52 |
53 |
54 |
55 |
56 |
57 |
| Composition of Treatment solution |
|
|
|
|
|
|
|
|
|
|
| H2SO4(mol/l |
- |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
- |
- |
- |
| SrSO4(mol/l) |
- |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
| Kind of Oxidizing Agent |
|
|
|
|
|
|
|
|
|
|
| Air (ml/min) |
- |
- |
- |
- |
50 |
- |
- |
- |
50 |
- |
| O2 (ml/min) |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
- |
| O3 (ml/min) |
- |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
| Na2ClO3 |
- |
o |
- |
- |
- |
- |
- |
o |
- |
- |
| Na2S2O8.2H2O |
- |
- |
o |
- |
- |
- |
- |
- |
- |
- |
| Discharge Capacity Ratio |
100 |
106 |
106 |
104 |
105 |
104 |
104 |
105 |
106 |
103 |
Table 7
| Sample No. |
1 |
58 |
59 |
60 |
61 |
62 |
63 |
64 |
65 |
66 |
| Composition of Treatment Solution |
|
|
|
|
|
|
|
|
|
|
| H2SO4 (mol/1) |
- |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
- |
- |
- |
| LaSO4 (mol/l) |
- |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
| Oxidizing Agent |
|
|
|
|
|
|
|
|
|
|
| Air (ml/min) |
- |
- |
- |
- |
50 |
- |
- |
- |
50 |
- |
| O2 (ml/min) |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
- |
| O3 (ml/min) |
- |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
| Na2ClO3 |
- |
o |
- |
- |
- |
- |
- |
o |
- |
- |
| Na2S2O8.2H2O |
- |
- |
o |
- |
- |
- |
- |
- |
- |
- |
| Discharge Capacity Ratio |
100 |
107 |
106 |
105 |
107 |
107 |
106 |
105 |
106 |
104 |
[0076] Tables 6, 7 and 8 show that all of the discharge capacity ratio obtained with EMD
powders on which surface modified layers are formed by a Sr and/or La compound and
a Sr and/or La compound containing Mn compound are higher than that obtained with
untreated EMD powder (Sample No.1), as improved discharge voltage.
[0077] In addition to these, a slight improvement of discharge capacity ratio is seen when
the treatment solution is acidified by H
2SO
4 and when an oxidizing agent of any type is employed although no obvious dependency
on the type of oxidizing agent is seen in this case also.
[0078] Like the cases of Embodiments -3 and -4, higher apparent densities are observed with
the EMD powders of which surfaces are modified by mixing a Mn compound in the layer.
Moreover, apparent from Fig. 7, since the heavy load discharge voltage of the cell
(Sample No. 58) employing the EMD powder of which surface is modified by La compound
is higher than that employing the untreated EMD powder (Sample No. 1), an increase
of discharge capacity up to a voltage of 0.9 V is seen. However, no particular difference
in the total capacity is observed.
Table 8
| Sample No |
1 |
67 |
68 |
69 |
70 |
71 |
72 |
73 |
74 |
75 |
76 |
| Composition of Treatment solution |
|
|
|
|
|
|
|
|
|
|
|
| H2SO4(mol/l) |
- |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
2.0 |
- |
- |
- |
| SrSO4(mol/l) |
- |
0.2 |
- |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
| LaSO4(mol/l) |
- |
0.2 |
0.2 |
- |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
| MnSO4(mol/l) |
- |
- |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
- |
0.2 |
| Kind of Oxidizing Agent |
|
|
|
|
|
|
|
|
|
|
|
| Air (ml/min) |
- |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
- |
| O2 (ml/min) |
- |
- |
- |
- |
- |
- |
- |
50 |
- |
- |
- |
| O3 (ml/min) |
- |
- |
- |
- |
- |
- |
- |
- |
50 |
- |
- |
| Na2ClO3 |
- |
o |
o |
o |
o |
- |
- |
- |
- |
- |
- |
| Na2S2O8.2H2O |
- |
- |
- |
- |
- |
o |
- |
- |
- |
- |
- |
| Apparent Density (g/cm-3) |
|
|
|
|
|
|
|
|
|
|
|
| |
2.67 |
2.63 |
3.01 |
2.97 |
2.92 |
2.92 |
2.95 |
3.0 |
3.01 |
2.64 |
2.84 |
| Discharge Capacity Ratio |
|
|
|
|
|
|
|
|
|
|
|
| |
100 |
105 |
105 |
105 |
106 |
107 |
106 |
107 |
105 |
103 |
103 |
[0079] All of the cells employing the other EMD powder of which surface is modified by another
Sr and/or La compound and by a Sr and/or La compound including the Mn compound showed
similar behaviors.
[0080] Fig. 8 shows a relationship between the pulse discharge cycle counts of LR6-size
alkaline manganese batteries employing the EMD powder of which surface is modified
by depositing a Sr and La compound as its positive active material and the total contents
of Sr and La. Fig. 8 shows also that all of the batteries employing EMD powder of
which surface is modified by a Sr and/or La compound show definite improvements of
pulse discharge cycle counts, and it is particularly effective when the total content
of Sr and/or La is in a range from 0.1 - 10.0 wt%.
[0081] In addition to this, an electron microscopic observation made on the EMD powder of
which surface modified by a Sr and/or La compound and a Sr and/or La compound containing
Mn compound have proved less surface irregularities like the other EMD powder of which
surface is modified. In addition to this, higher apparent densities with the surface
modified EMD powders containing Mn compound (Sample Nos. 68 -74 and 76) is obtained
like the other cases.
<Embodiment-6>
[0082] The performance of the positive active material developed for non-aqueous electrolyte
secondary batteries of Sample Nos. 1 - 76 shown in Embodiments -1 - -5 have been tested.
[0083] A cross-section of coin type cell developed for the evaluation of invented positive
electrode is shown in Fig. 9 wherein 21 is a cell-case made of stainless-steel anti-corrosive
to the organic electrolyte, 22 is a cell cover made of the same material, 23 is an
invented positive electrode, 24 is a current collector for positive electrode 23 made
of the same stainless-steel and is spot-welded to the internal surface of cell-case
21, 25 is negative electrode molded graphite powder and pressed against the inside
of cell cover 22. 26 is a separator made of porous polypropylene, and 27 is an insulating
gasket made of polypropylene. The evaluation cell coin type has a diameter of 20 mm
and an overall height of 1.5 mm.
[0084] The positive active material is prepared by mixing various surface modified EMDs
prepared in advance with lithium hydroxide (LiOH) at a ratio forming a double oxide
of manganese and lithium, LiMn
2O
4 of prescribed composition, and this mixture is sintered at a temperature of 860°C
for 70 hours in an oxidizing atmosphere. The positive electrode compound is prepared
by mixing a conductive agent into polyvinylidenfluoride acting as a binder at a weight
part of 5 to 5, and by mixing this mixture into the obtained positive active material
at a weight part of 90. Preparing the electrode by molding thus obtained positive
electrode compound of a -prescribed volume on current collector 24, this is dried
at a temperature of 150°C in vacuum condition, and this is assembled into a cell using
a negative electrode 25.
[0085] As an electrolyte, lithium perchlorate dissolved in a solvent where ethylene carbonate
and 1, 3-dimethoxyethane are mixed at an equal volume obtaining a concentration of
1 mol/litter is used. Since positive electrode is deintercalated lithium-ions electrochemically
to electrolyte by charging after the cell assembly, and intercalated the lithium ions
from electrolyte by discharging, it is obvious that this functions as a positive electrode
material for secondary batteries.
[0086] These evaluation cells were charged up to a voltage of 4.2 V at a rate of 0.2 mA/cm
2, and then discharged to a voltage of 3.0 V at a rate of 0.2 mA/cm
2 and 1.0 mA/cm
2 at an ordinary temperature, and the discharge characteristics depending on the difference
of discharge rate have been determined.
[0087] Table 9 shows the ratio of discharge capacity at a rate of 1.0 mA/cm
2 to that at a rate of 0.2 mA/cm
2.
[0088] In here, the tests are conducted for Sample Nos. S-2, -9, -13, -14, -22, -31, -50,
and -59 employing a concentration of sulfuric acid of 2.0 mol/l and a concentration
of various sulfate of 0.2 mol/l as a condition of surface modification treatment,
and employing sodium perchlorate as an oxidizing agent, the results of these are compared
with that of EMD powder of Sample No. S-1 used as a starting material.
Table 9
| Sample No. |
S-1 |
S-2 |
S-9 |
S-13 |
S-14 |
S-22 |
S-31 |
S-50 |
S-59 |
| Discharge Capacity Ratio(%) |
88 |
93 |
89 |
92 |
92 |
91 |
91 |
90 |
90 |
[0089] As shown in Table 9, the surface modified samples show better high-rate discharge
characteristics than the one obtained by the referenced sample No.S-1. Moreover, the
same effects could be obtained if the surface modification were made on the samples
mentioned other than the above.
<Embodiment-7>
[0090] Using the materials of Sample Nos. 1 - 76 shown in Embodiemnts-1 -5 as a positive
active material and zinc as a negative active material, the zinc chloride type carbon-zinc
dry cells shown in Fig. 10 are prepared.
[0091] In Fig. 10, 31 is a positive electrode mix, 32 is a carbon rod acting as a positive
current collector, 33 is a zinc can, 34 is a separator, 34A is a bottom paper, 35
is a plastic sealing cover, 35A is a positive terminal plate, 36 is a cover paper,
36A is sealer, 37 is a negative terminal plate, 38 is a PVC tube, and 39 is a metal
jacket. Positive electrode mix 31 is prepared by mixing said manganese dioxide with
acetylene-black at a weight ratio of 5 : 1, by mixing this into an electrolyte consisting
of zinc chloride and ammonium chloride mixed solution, which main constituent is zinc
chloride, and by molding.
[0092] R20 (D) size carbon-zinc dry cells are prepared thus, and these are continuously
discharged for a load of 2 Ohms at room temperature (20°C), and the end voltage is
down to 0.9 V. The results of these are shown in Table 10.
Table 10
| Sample No. |
1 |
2 |
5 |
12 |
13 |
14 |
24 |
33 |
52 |
61 |
| Discharge Duration Ratio |
100 |
106 |
105 |
105 |
104 |
105 |
104 |
105 |
104 |
104 |
[0093] As shown in Table 10, carbon-zinc dry cells show better heavy-load discharge characteristics
when a manganese dioxide having a surface modified layer is employed over the cases
where the cells employ a manganese dioxide having a unmodified surface layer.
[0094] Taking an example for mainly an alkaline manganese battery prepared by employing
an EMD powder having a surface modified layer by compound consisting mainly of oxide
of at least one element selected out of a group of Ti-, Co, Ni, Sr, and La, and is
used as the positive active material, the resistance polarization and the concentration
polarization are obviously lowered at the heavy load and continuous discharge so that
discharge characteristics of high efficiency can be obtained by the increased discharge
voltage and the effective capacity.
Those cases wherein a Mn compound is introduced in the surface modified layer are
found effective also.
[0095] The effects available with the above-mentioned surface layer modification are not
necessarily be limited to the alkali manganese batteries only. By conducting a surface
modification depositing a compound of at least one element selected out of a group
of Ti, Co, Ni, Sr, and La on the surface of not only EMD but CMD and natural manganese
dioxide (NMD), and by using this as a positive active material, those can be applied
to Leclanche type and zinc chloride type carbon-zinc dry batteries also.
[0096] Moreover, by applying a heated dehydration treatment at a temperature from 350 -
450°C to said surface modified manganese dioxide powder, the positive active material
for the Li/MnO
2 system organic electrolyte lithium primary battery having a high rate discharge characteristics
can be obtained.
[0097] Furthermore, by using a manganese oxide on which a surface modified layer is formed
by depositing a compound of at least one element selected out of a group of Ti, Co,
Ni, Sr, and La on the surface of LiMnO
2 or LiMn
2O
4 powder which is a double oxide of Mn and Li repeating the deintercalation and intercalation
of Li by charge and discharge as the positive electrode, still-better charge and discharge
characteristics can be obtained.
[0098] In these embodiments, although an example using a sulfate aqueous solution as the
treatment solution for surface modification has been shown, the treatment solution
of this invention in not necessarily be limitedwithin the usage of sulfates.
[0099] That is, when chlorides or nitrates etc, are used as the positive active material
of the battery after the treatment, the use of these salt can never be disturbed by
the possible introduction of minute anions contained in the treatment solution. For
instance, it could be well understood that the use of chloride solution as the treatment
solution acting as the positive active material for carbon-zinc dry batteries wherein
NH
4Cl and/or ZnCl
2 is used as an electrolyte.
[0100] This invention is to offer batteries using a manganese oxide on which the surface
of manganese oxide powder consisting of MnO2, Mn and Li of a double oxide is modified
by the deposition of a compound consisting mainly of an oxide of at least one element
selected out of a group of Ti, Co, Ni, Sr, and La as its positive active material
and a compound made mainly of a Mn oxide by using a solution dissolving a salt of
at least one element selected out of a group of Ti, Co, Ni, Sr, and La to which a
Mn salt is added.
[0101] And this is highly effective to improve the heavy load continuous discharge characteristics
of primary batteries such as carbon-zinc dry batteries, alkaline manganese batteries,
and Li/MnO
2 system organic electrolyte lithium batteries.
[0102] Furthermore, further improvements of high-rate charge and discharge characteristics
with the lithium-ion secondary batteries can be expected also. These could be possible
by the reduction of resistance polarization and/or concentration polarization of the
positive active material used therein.